[0001] The present invention relates to a process for manufacturing a material including
polyurethane and to the material thus obtained.
[0002] In addition, the present invention relates to use of silica and/or treated silica
in a process for preparing polyurethane materials.
[0003] It is known that polyurethane-including materials form a very important class of
polymeric materials presently available on the market within the wide field of synthetic
materials.
[0004] Polyurethane-including materials find application in many technical fields, for instance
polyurethane materials are employed in producing: fibres, resins for coating, elastomer
materials, foamed materials and others.
[0005] The wide diffusion of the polyurethane materials is due to the particular features
owned by the "polyurethane" polymer.
[0006] Polyurethane is a repetition of urethane monomers (carbamic ester) and is usually
obtained by poly-addition reactions.
[0007] Polyurethane can take a structure formed of straight polymeric chains (thermoplastic
materials) or alternatively it can take a structure in which the polymeric chains
are disposed to form a tridimensional crystalline structure (thermosetting materials)
.
[0008] In particular thermoplastic polyurethanes can be employed in preparing foamed materials.
Foamed thermoplastic materials have reduced density values as compared with unfoamed
compact thermoplastic polyurethanes.
[0009] Foamed materials and in particular polyurethanes, widely apply in all sectors in
which articles of reduced specific weight are to be produced at low costs.
[0010] Among the techniques employed for expanding a thermoplastic polyurethane, use of
water, CO
2 or foaming chemical compounds of various nature can be provided. Depending on the
quality and amount of the foaming agents employed, polyurethane materials having different
density values are obtained.
[0011] While different technologies and processes are available for manufacturing foamed
materials, the foamed thermoplastic polyurethanes presently on the market appear to
be unsuitable to meet applications where a high geometry observance and tolerance
control is required as well as an excellent observance of the surface finish.
[0012] Practically, the density value of a thermoplastic polyurethane material can be modified
with ease but the foamed materials thereby obtained do not yet possess physical, chemical
and mechanical features allowing the same to meet specific tolerance and finish requirements.
[0013] With reference to a conventional moulding process of a thermoplastic polyurethane
material, some possible causes of the above-highlighted properties of the foamed materials
will be briefly analysed hereinafter.
[0014] To give an example of a process for preparing a moulded article, it is known that
a thermoplastic polyurethane material in any physical form thereof, in the form of
a granule for example, is charged into a mixing means, a single-screw or multi-screw
feeder for example.
[0015] Subsequently to the material-charging step, foaming agents are mixed therewith to
a pre-established temperature, to form a mixture.
[0016] Following a mechanical mixing operation, the mixture consisting of thermoplastic
polyurethane and foaming agent softens until it melts. At the instant that the thermoplastic
polyurethane, in the form of a granule for example, melts, the foaming agent too reacts.
[0017] At this step the foaming process of the thermoplastic polyurethane material begins
and propagates.
[0018] Subsequently, the melted thermoplastic polyurethane mixture is injected into the
mould that will give the desired article its final shape.
[0019] Many problems are encountered in a process of the type described above. A first drawback
is given by the fact that during the mixing and stirring step strong rubbing actions
and frictions are created so that the mixture temperature rises, which will make it
very difficult to carry out a thermal control during this stirring and mixing step.
[0020] A difficult thermal control during the step of treating the mixture comprising thermoplastic
polyurethane and foaming agents causes a non-homogeneous expansion process of the
material.
[0021] Practically, a disorderly and non-uniform expansion process takes place in the whole
mixture. Due to lack of a sufficient thermal control, reaction of the foaming agents
occurs in a short period of time which will cause localized sharp reactions within
the mass being processed.
[0022] For the above reason, the foamed thermoplastic material has porous regions alternated
with regions full of true cavities of different sizes. In addition, the foaming process
duration can be hardly foreseen and sometimes it can go on during the moulding step
too.
[0023] A second drawback is given by the fact that the thermoplastic polyurethane material
has a very tenacious molecular structure tending to resist the foaming process. The
intrinsic resistance that the polymeric material shows against the foaming process
produces a material in which the polymeric chains have been submitted to strong stretching
stresses.
[0024] Therefore, the foamed thermoplastic polyurethane mass shows unevenness in the distribution
of the microporosities present therein, as well as in the sizes of the individual
porosities and in the distribution of inner stresses.
[0025] It is obvious that the above gives rise to a further drawback resulting from the
necessity to utilise high pressures during the step of injecting the molten material
into the mould for the purpose of obtaining an at least acceptable quality of the
finished work.
[0026] Therefore, there is a need for a thermoplastic polyurethane material free of the
drawbacks of the known art.
[0027] In particular it is one aim of the present invention to provide a process for manufacturing
a polyurethane material preferably of the thermoplastic type which can be foamed in
a controlled and uniform manner and at the desired foaming degree depending on the
intended uses.
[0028] Another aim of the invention is to obtain a thermoplastic material having the above
described features and adapted to be used in a moulding operation giving rise to articles
of very high quality in terms of surface finish and geometric observance of the tolerances.
[0029] The foregoing and further aims that will become apparent during the following detailed
descriptions have been achieved by the Applicant that has found it useful to employ
a particular additive in a technological preparation process of a thermoplastic polyurethane
material.
[0030] In particular, the Applicant has surprisingly selected a particular type of oxide
from the additives.
[0031] It is therefore a first objet of the present invention to provide a process for manufacturing
a polymeric material including a thermoplastic polyurethane the essential features
of which are set out in the appended independent claim.
[0032] Other preferred embodiments are described in the appended dependent claims.
[0033] Further technical features and the advantages of the invention will be best understood
from the following detailed description.
[0034] For carrying out preparation of the thermoplastic polyurethane material, reaction
of at least one first and one second reactant is provided, the features of these reactants
being better detailed below.
[0035] In particular, the first reactant contains isocyanate functional groups capable of
reacting with the hydroxyl functional groups contained in the other reactant.
[0036] Preferably said first reactant can be in the form of a monomer or in a partly reacted
form, without obviously limiting the invention scope.
[0037] Said first reactant can be in any physical form provided its reactivity is not limited.
[0038] For instance, said first reactant can be in a liquid or dispersed form. Advantageously,
said first reactant may comprise charges, additives and/or filling materials which
in turn may be in a liquid or solid form, commonly employed in this specific technical
field.
[0039] For example, said first reactant can be a diisocyanate of general formula O=C=N-R-N=C=O,
a triisocyanate of general formula O=C=N-R(-N=C=O)
2; wherein R can be an aromatic and/or alkyl group or chain, without limiting the invention
scope at all.
[0040] The second reactant contains hydroxyl functional groups capable of reacting with
the isocyanate functional groups contained in the first reactant.
[0041] Preferably, said second reactant can be in the form of a monomer or in a partly reacted
form.
[0042] Said second reactant can be in any physical form provided its reactivity is not limited.
[0043] For instance, said second reactant can be in a liquid or dispersed form. Advantageously,
said second reactant may include charges, additives and/or filling materials which
in turn may be in a liquid or solid form, commonly employed in this specific technical
field.
[0044] For example, said second reactant can be a glycol of general formula H-O-R-O-H, wherein
R can be an aromatic and/or alkyl group or chain; an organic and/or alkyl divalent
alcohol; an organic and/or alkyl trivalent alcohol without limiting the invention
scope at all.
[0045] The process comprises a reaction step between a first reactant, containing isocyanate
functional groups and a second reactant containing hydroxyl functional groups. Clearly
the order according to which the two reactants are mixed with each other or possibly
with other additives in the reaction step depends on the usual procedure well known
to those skilled in the art.
[0046] Advantageously, the reaction step between the two reactants can be conducted following
various operating modalities involving use of reactor means, reaction times, reaction
temperatures and mixing steps usually employed by those skilled in the art.
[0047] Generally, said reaction step between the two reactants leads to formation of a polymeric
material that preferably will have a straight structure (thermoplastic material).
[0048] The process being the object of the invention comprises at least one further step
involving silica addition.
[0049] In a first preferred embodiment of the process, silica is added to said first reactant
prior to said reaction step.
[0050] In a second preferred embodiment of the process, silica is added to said second reactant
prior to said reaction step.
[0051] In a third preferred embodiment of the process, silica can be also added during the
reaction step between said first and second reactants.
[0052] In particular, the first and second reactants, typically in a liquid phase, can be
provided to be associated and mixed with each other with addition of the desired amounts
of silica, in a conventional single-screw or multi-screw feeding and mixing device.
[0053] In a fourth preferred embodiment of the process, silica is added subsequently to
the reaction step between said first and second reactants. In this case it may be
provided for the thermoplastic granule to be brought to the melting temperature and
then silica is added.
[0054] Silica or silicon monoxide that is used in the process of the invention can be either
of natural origin (cristobalite, tridymite, low quartz, high quartz) or of synthetic
origin and in addition it can have an amorphous, crystalline or colloidal structure.
[0055] Preferably silica herein employed is a hydrophobic silica.
[0056] The Applicant in the process of the invention has found it particularly advantageous
to use silica in the form of compounds of treated silica. Practically, there are some
treatments in which the silica surface is completely coated with particular treatment
agents such as fluid silicone, silanes or silicone derivatives and others. The treatment
agent modifies the silica surface nature from hydrophilic to hydrophobic.
[0057] A first example of treated silica is given by the compound CAB-O-SIL® TS-720 (Treated
fumed silica; Cabot Corporation). It is a silica compound treated with fluid dimethyl
silicone. Treatment makes silica very hydrophobic.
[0058] A second example of treated silica is given by the compound CAB-O-SIL® TS-610 (Treated
fumed silica; Cabot Corporation). It is a silica compound treated with dimethyl chlorosilane.
Treatment makes silica very hydrophobic.
[0059] A third example of treated silica is given by the compound CAB-O-SIL® TS-530 (Treated
fumed silica; Cabot Corporation). It is a silica compound treated with hexamethyl
disilazane (HMDS, CAS: 999-97-3). Treatment makes silica very hydrophobic.
[0060] Use of silica in the form of particles and in particular micronized pyrogenic silica
or synthetic silicon dioxide amorphous to X rays is particularly advantageous.
[0061] It is pointed out that all the above mentioned silica types are silica examples finding
valid application for the purposes of the present invention.
[0062] Silica is homogeneously distributed in the thermoplastic polyurethane mass in the
form of fibres, powders, granules, aggregates and chains.
[0063] The silica amount that can be employed in the process of the invention greatly varies
depending on the type of polymeric material to be obtained.
[0064] Practically, the material containing thermoplastic polyurethane and silica can be
employed without limitations as an unfoamed compact polyurethane material or alternatively
it can be employed as a polyurethane material to be subsequently foamed by use of
appropriate foaming agents.
[0065] Preferably, silica can be employed in a concentration by weight included between
0.1 and 10% with respect to the total weight of the thermoplastic polyurethane material
and silica; more preferably in a concentration included between 0.1 and 5%.
[0066] Advantageously, the process of the invention may comprise further steps enabling
the material containing polyurethane and silica and possibly other additives to be
obtained in the form of granules or pellets as a raw material for subsequent mechanical-working
operations.
[0067] Alternatively, the process may comprise at least one step of adding at least one
foaming agent to said polyurethane material.
[0068] It is a second object of the present invention to provide a thermoplastic polymeric
material including polyurethane, the essential features of which are set out in the
appended independent claim.
[0069] Other preferred embodiments of said material are described in the appended dependent
claims.
[0070] Preferably, the polymeric material may also comprise additives, filling charges and
dyes.
[0071] The thermoplastic polyurethane material being the object of the present invention
comprises silica.
[0072] Preferably, said silica can be either of natural origin (cristobalite, tridymite,
low quartz, high quartz, for example) or of synthetic origin and in addition it can
have an amorphous, crystalline or colloidal structure.
[0073] Advantageously the polymeric material being the object of the present invention comprises
silica in the form of treated-silica compounds as previously described.
[0074] Use of micronized pyrogenic silica or synthetic silicon dioxide amorphous to X rays
appears particularly advantageous.
[0075] The polyurethane material comprises a varying silica amount depending on the type
of polymeric material to be obtained.
[0076] Preferably, silica can be employed in a concentration by weight included between
0.1 and 10% with respect to the total weight of the polyurethane material and silica;
more preferably, in a concentration included between 0.1 and 5%.
[0077] Silica, in the form of very thin and lightweight fibre for example, behaves like
a lubricant for the thermoplastic polyurethane polymeric chains. Practically, the
polyurethane chains slide on each other due to the presence of silica and consequently
during a foaming process they offer less resistance to stretching. The obtained polyurethane
material is less stressed. A material having these features can be melted and injected
into a mould to obtain a moulded article of the desired shape.
[0078] Alternatively, the material comprising thermoplastic polyurethane and silica can
be foamed with appropriate foaming agents. In the last-mentioned case the foaming
agents do not find a rigid molecular structure offering resistance to the foaming
process, because the presence of silica enables better sliding of the polymeric chains.
[0079] The particular types of silica employed by the Applicant enable foamed polyurethane
materials to be for example obtained which have a density value included between 0.2
and 1.2 g/cm
3; preferably between 0.3 and 1.1 g/cm
3; more preferably a density value ranging from 0.4 to 0.8 g/cm
3.
[0080] It is a further object of the present invention to provide use of silica in processes
for manufacture of thermoplastic polyurethane materials as set out in the appended
independent claim.
[0081] Other preferred embodiments concerning use of silica in a process for manufacturing
a polyurethane material are described in the appended dependent claims.
[0082] Preferably, the silica or silicon oxide used in the processes for manufacturing thermoplastic
polyurethane materials can be either of natural origin (cristobalite, tridymite, low
quartz, high quartz, for example) or of synthetic origin and in addition it can have
an amorphous, crystalline or colloidal structure.
[0083] Preferably silica employed in the present invention is a hydrophobic silica.
[0084] The Applicant in the process of the invention has found it particularly advantageous
to use silica in the form of compounds of treated silica. Practically, there are some
treatments in which the silica surface is completely coated with particular treatment
agents such as fluid silicone, silanes or silicone derivatives and others. The treatment
agent modifies the silica surface nature from hydrophilic to hydrophobic.
[0085] A first example of treated silica is given by the compound CAB-O-SIL® TS-720 (Treated
fumed silica; Cabot Corporation). It is a silica compound treated with fluid dimethyl
silicone. Treatment makes silica very hydrophobic.
[0086] A second example of treated silica is given by the compound CAB-O-SIL® TS-610 (Treated
fumed silica; Cabot Corporation). It is a silica compound treated with dimethyl chlorosilane.
Treatment makes silica very hydrophobic.
[0087] A third example of treated silica is given by the compound CAB-O-SIL® TS-530 (Treated
fumed silica; Cabot Corporation). It is a silica compound treated with hexamethyl
disilazane (HMDS, CAS: 999-97-3). Treatment makes silica very hydrophobic.
[0088] Use of silica in the form of particles and in particular micronized pyrogenic silica
or synthetic silicon dioxide amorphous to X rays is particularly advantageous for
preparation of polyurethane materials.
[0089] The silica amount that can be employed in a process for manufacturing thermoplastic
polyurethane materials may vary depending on the type of polymeric material to be
obtained.
[0090] Preferably, for manufacturing thermoplastic polyurethane materials, silica is employed
in a concentration by weight included between 0.1 and 10% with respect to the total
weight of the thermoplastic polyurethane material and silica; more preferably in a
concentration included between 0.1 and 5%.
[0091] It is a further object of the present invention to provide use of a polymeric material
including thermoplastic polyurethane and silica in a process for manufacturing a foamed
material, as set out in the appended independent claim.
[0092] Use of a polymeric material comprising thermoplastic polyurethane and silica appears
advantageous in a moulding process of a foamed material, a thermoplastic foamed polyurethane
material for example.
[0093] The Applicant in the practical application of the present invention has found a series
of advantages that are reproduced hereinafter.
[0094] A first advantage resides in that a material comprising thermoplastic polyurethane
and silica, during the moulding step for example, has a very high injection speed
enabling use of controlled forces and pressures that can be easily reached with traditional
machinery.
[0095] A second advantage is given by the fact that the material comprising polyurethane
and silica can be submitted to aesthetic-finish steps and dyeing steps to obtain articles
of excellent finish and good commercial value.
[0096] A further advantage resides in that the material comprising polyurethane and silica
has a good dimensional stability and elastic properties, is light in weight, has a
good resistance to wear and can be recycled.
[0097] A still further advantage of a material comprising polyurethane and silica is given
by the fact that if it is submitted to a foaming process its expansion takes place
in a gradual and uniform manner without causing sharp expansion reactions within the
mass under foaming.
[0098] Finally, the material being the object of the present invention can be employed for
obtaining a wide variety of foamed materials to be put on the market as an alternative
in order to replace foamed PVC and foamed thermoplastic rubbers.
1. A process for manufacturing a polyurethane-including polymeric material comprising
a reaction step between a first reactant containing isocyanate functional groups and
a second reactant containing hydroxyl functional groups, both said reactants being
capable of reacting with each other to define a predetermined amount of polyurethane
material, characterized in that said process comprises at least one further step involving silica addition.
2. A process as claimed in claim 1, characterized in that silica is added to said first reactant.
3. A process as claimed in claim 1 or 2, characterized in that silica is added to said second reactant.
4. A process as claimed in one or more of the preceding claims, characterized in that silica is added during the reaction step between said first and second reactants.
5. A process as claimed in one or more of the preceding claims, characterized in that silica is added subsequently to the reaction step between said first and second reactants.
6. A process as claimed in one or more of the preceding claims, characterized in that silica is of natural or synthetic origin.
7. A process as claimed in claim 6, characterized in that silica has an amorphous, crystalline or colloidal structure.
8. A process as claimed in one or more of the preceding claims, characterized in that silica is in the form of treated-silica compounds.
9. A process as claimed in claim 8, characterized in that the treated silica is silica coated with treatment agents modifying the silica surface
nature from hydrophilic to hydrophobic.
10. A process as claimed in one or more of the preceding claims, characterized in that silica is a micronized pyrogenic silica or synthetic silicon bioxide amorphous to
X rays.
11. A process as claimed in one or more of the preceding claims, characterized in that silica is added in a concentration included between 0.1 and 10% by weight with respect
to the total weight of the polyurethane material and silica.
12. A process as claimed in one or more of the preceding claims characterized in that it comprises at least one step of adding at least one foaming agent to said polyurethane
material.
13. A process as claimed in one or more of the preceding claims, characterized in that said polyurethane material is a thermoplastic material.
14. A polyurethane-including polymeric material characterized in that it comprises silica.
15. A material as claimed in claim 14, characterized in that silica is of natural or synthetic origin.
16. A material as claimed in claim 14 or 15, characterized in that silica has an amorphous, crystalline or colloidal structure.
17. A material as claimed in one or more of the preceding claims, characterized in that silica is in the form of treated-silica compounds.
18. A material as claimed in claim 17, characterized in that the treated silica is silica coated with treatment agents modifying the silica surface
nature from hydrophilic to hydrophobic.
19. A material as claimed in one or more of the preceding claims, characterized in that said silica is homogeneously distributed in the polyurethane material mass in the
form of particles, preferably fibres, powders or granules.
20. A material as claimed in one or more of the preceding claims, characterized in that silica is a micronized pyrogenic silica or synthetic silicon bioxide amorphous to
X rays.
21. A material as claimed in one or more of the preceding claims, characterized in that silica is in a concentration included between 0.1 and 10% by weight with respect
to the total weight of the polyurethane material and silica.
22. A material as claimed in one or more of the preceding claims, characterized in that it comprises at least one foaming agent.
23. Use of silica in a process for manufacturing polyurethane materials.
24. Use of a polymeric material comprising polyurethane and silica according to one or
more of claims 14 to 22, in a process for manufacturing a foamed material.
25. Use of a polymeric material as claimed in claim 24, in a moulding process of foamed
materials.
26. Use as claimed in claim 24 or 25 characterized in that said foamed material is a thermoplastic polyurethane.